JPS59199863A - Production of surface modified substance - Google Patents

Production of surface modified substance

Info

Publication number
JPS59199863A
JPS59199863A JP7223183A JP7223183A JPS59199863A JP S59199863 A JPS59199863 A JP S59199863A JP 7223183 A JP7223183 A JP 7223183A JP 7223183 A JP7223183 A JP 7223183A JP S59199863 A JPS59199863 A JP S59199863A
Authority
JP
Japan
Prior art keywords
polymerization
solution
modified
immersed
catalyst
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7223183A
Other languages
Japanese (ja)
Inventor
別田 安弘
堀家 茂樹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shinwa Seisakusho Co Ltd
Original Assignee
Shinwa Seisakusho Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shinwa Seisakusho Co Ltd filed Critical Shinwa Seisakusho Co Ltd
Priority to JP7223183A priority Critical patent/JPS59199863A/en
Publication of JPS59199863A publication Critical patent/JPS59199863A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は表面が自由に接触しあって℃・る粗粒砂、lp
維、繊(、fn毛などの表面に各々の粒子、単Ip翔な
どを接シ1qさせることな(合成樹脂を核種させること
により粗粒砂、繊維毛などの表面を改質する方法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is characterized in that coarse-grained sand, lp
Concerning a method for modifying the surface of coarse sand, fiber hair, etc. by making a synthetic resin a nuclide without contacting the surface of fibers, fibers (, fn hair, etc.) with individual particles, single IP, etc. It is.

従来、素材がポリエステルなどの合成%i(KJi毛は
獣毛に較べて親水性が乏しく合成線ΔM毛を累月として
試作した毛准は墨の含みが悪く筆記中に墨切れが頻繁で
実用に供し得な(・、然しポリエステル繊維毛はヤング
率などでみれば明瞭な如く獣毛と較べて腰が強(、これ
を蔽素材とした場合には腰の強い壬良記し易し・毛燈と
なる捨て難〜・長所を有している。
Conventionally, the material was synthetic %i such as polyester (KJi hair was less hydrophilic than animal hair, and the synthetic line ΔM hair was prototyped as a comb), which did not hold ink well and frequently broke ink while writing, making it unsuitable for practical use. (・However, polyester fiber wool has a stronger elasticity than animal hair, as is clear from Young's modulus.) It has the advantage of being a light that cannot be thrown away.

従ってポリエステル繊維毛に親水性を耐力すべくポリア
ミド4酊月旨、セルロース+ivt ++旨、蛋白質な
どの揮発性溶媒による浴液又は自己硬化型樹脂溶液を塗
布して乾燥固化した場合、各単繊維同、dが膠着した繊
維毛の塊りが形成されてしまう、このことは繊維毛表面
に樹力旨層が形成される限りは如何に樹脂溶液の濃度を
稀薄なものとしても各単faH’J同志の膠着は避ける
ことか出来す、逆に該繊維質を溶′A’Jぜず膠着した
組ル又のみを醪解する溶を色で完全に膠着を解くまで洗
浄すると繊維毛表面に形成された合成樹脂層までも洗い
流されてしまうことは周知の基本原理である。
Therefore, in order to make polyester fibers hydrophilic, if a bath liquid or a self-curing resin solution containing a volatile solvent such as polyamide 4, cellulose, or protein is applied and dried and solidified, each single fiber will be the same. , d will form a clump of stuck fiber hairs.This means that no matter how dilute the resin solution concentration is, each monofaH'J It is possible to avoid adhesion of the comrades.Conversely, if you wash the fibers with color until the adhesion is completely dissolved, it will form on the surface of the fibers. It is a well-known basic principle that even the synthetic resin layer that has been washed away will be washed away.

本発明は以上の諸点を考慮したものであり、局分子でな
℃・重合触媒は表面が自由に接触し合っている繊に41
毛などの表面に各4繊維同志を膠着することなく存在さ
せることが出来、重合は触媒の存在するところに於ての
み進行し、触媒は単量体又は単杭体溶液中にみだりに浸
出したり移行したつせづ“、正合は不均一系で進行する
と云う前提条件のもとに各単繊維同志な)遥着すること
なく繊維毛表面に合成樹脂層を形成させることにより該
X:i維毛表面を改質する方法を提供するものである。
The present invention takes the above points into consideration, and the polymerization catalyst, which is not a local molecule, is applied to the fibers whose surfaces are in free contact with each other at 41°C.
Each of the four fibers can be present on the surface of hair etc. without sticking to each other, and polymerization will proceed only where the catalyst is present, and the catalyst will not be leached into the monomer or single pile solution. Based on the premise that the transferred mating progresses in a non-uniform system, the X:i The present invention provides a method for modifying the surface of hair fibers.

更に本発明による方法は維単に合成繊維毛の表向に親水
性を附Jiする為の方法でばなく、逆に親油性(疎水性
)を附与することによりγ11性塗料用の犀、刷毛索胴
とする方法及び合成樹脂り層を形成させる対象が繊維毛
のみではなくフンタクトレンズ、フィルム、シート箔、
球、顆粒砂などの辿範の塗装方法では各構成単位同志が
接着し、K’s 71.”i してしまうようなものの
表面に合成樹脂層ケ形tAさせることにより表面を改質
する方法乞も示唆するものである。
Furthermore, the method according to the present invention is not only a method for imparting hydrophilicity to the surface of synthetic fiber bristles for the purpose of textiles, but also a method for imparting lipophilicity (hydrophobicity) to the surface of synthetic fibers. The method of forming a cable trunk and the object of forming a synthetic resin layer are not only fibers but also lenses, films, sheet foils, etc.
In traditional painting methods such as spheres and granular sand, the constituent units adhere to each other, resulting in K's 71. The present invention also suggests a method of modifying the surface of a material that would otherwise be damaged by forming a synthetic resin layer on the surface.

以下、本発明の技術内容を実験により他、認し1こ実施
例にもとづき説明すると合成繊維毛素材としては獣毛の
ように先端をテーパー状に先鋭化したポリエステル繊維
毛で長さが50ミリメートル、根元の太さが2.5ミル
の直径約50ミリメートル繊維毛東を使用し、表面に附
与する合成樹脂層としては親水性ポリアミドとして新た
に開発された組織名ポリテトラヒドロビラン−2,6−
ジイルイ5ノカルボ0ルなるポリ双環シーキサラクタム
でイヒ学構造は次のようになる 該ポリ双環オキサラクタムは組織名8−オキサ−6−7
サヒシクq [3,2,1,:)オクタン−7−オンな
る次に示す化学構造の双環オキサラクタムを単量体とし
て7ニオン的に重合したものである重合方法及び得られ
たポリ双環オキサラクタムの詳細な説明は、住友宏「親
水性の新しく・ナイロン」工朶拐科第29巻第8号23
貞(1981) 、又は住友宏「親水性ポリアミドj模
」腺ちシ保全と(Iト化の化学193頁、東冨犬学出版
会(1981)などeこlj?1示され一ζいる。
The technical content of the present invention will be explained based on experiments and examples below.The synthetic fiber hair material is polyester fiber hair with a tapered tip like animal hair and has a length of 50 mm. A fiber with a diameter of about 50 mm with a base thickness of 2.5 mil is used, and the synthetic resin layer added to the surface is made of polytetrahydrobilane-2,6, a newly developed hydrophilic polyamide. −
This polybicyclic oxalactam is a polybicyclic oxalactam, which has the following structure:
Polymerization method and resulting polybicyclic polymerization method in which bicyclic oxalactam having the chemical structure shown below, which is sahishikq [3,2,1,:)octan-7-one, is polymerized in a 7-ion manner as a monomer. For a detailed explanation of oxalactam, please refer to Hiroshi Sumitomo, “New Hydrophilic Nylon,” Engineering Research, Vol. 29, No. 8, 23.
Sada (1981), or Hiroshi Sumitomo, ``Hydrophilic Polyamide Model'', ``Hydrophilic Polyamide Model'', ``Hydrophilic Polyamide Preservation'' (193 pages of Itoka no Chemistry, Higashifugaku Publishing Co., Ltd. (1981), etc.) have been shown.

重合触媒としては開始剤と活性化剤とがあり、1、Ii
1始剤としては乾燥窒素気流下でテトラヒドコ7クタム
のカリウム塩で次の化学構造で示される活性化剤として
は上記、双環オキサラククムのN−アセチル化物を用い
た、化学構造は次の辿りである    O 単量体、開始剤、活性化テ■すの合成及び精製方法は住
友宏、橋本和診、マクロモレクルス、第10号1327
貞(1977)に示されたあ法を基本的に用℃・た。
Polymerization catalysts include initiators and activators, and 1.Ii
The first initiator was the potassium salt of tetrahydrococctam under a stream of dry nitrogen, and the activator was the N-acetylated product of bicyclic oxalaccum, as shown in the following chemical structure. Synthesis and purification methods for certain O monomers, initiators, and activation materials are described by Hiroshi Sumitomo, Washin Hashimoto, Macromolecules, No. 10, 1327.
I basically used the method shown in Sada (1977).

実施例 乾燥窒素気流下で合成し、封管中に保存した正+1i3
2(1!Jグラムの開始剤址に合わせて開始剤濃度が単
量体に対して2モルパーセントとなるように13.6グ
ラムの単量体をナスフラスコに秤取し、室温で脱気及O
・乾燥窒素置換をに、#+り返した後ドライボックス中
に持込む、ドライボックス中にはこの他にvl」始剤で
ある触媒の入った封管、活性化Allの入った螺子栓谷
器、ポリエステル繊維毛束、溶媒の入った螺子栓谷器、
その他操作に必要な器μ類を持込み、一旦水銀柱2ミリ
メートル以下に1時間以上脱気後、乾は窒素て置換し、
以下の操作はニー゛ライボックス中で行う。
Example Positive +1i3 synthesized under a stream of dry nitrogen and stored in a sealed tube
Weigh out 13.6 grams of monomer into an eggplant flask so that the initiator concentration is 2 mole percent based on the monomer, and degas at room temperature. O
・After repeating the dry nitrogen purge, bring it into the dry box.In addition to this, the dry box contains a sealed tube containing a catalyst, which is an initiator, and a screw stopper containing activated All. container, polyester fiber bundle, screw cap container containing solvent,
Bring in other equipment necessary for the operation, degas it to less than 2 mm of mercury for more than 1 hour, and then replace the drying with nitrogen.
The following operations are performed in the knee box.

100ミリリツトルビーカーに単辻体粉末を移し、33
.4ミリリツトルのテトラヒドロフランに溶解スるとと
もにマイクロシリンジを用いて165マイクロリツトル
の活性化剤を加えて早11一体浴液とする、次で触媒(
開始剤)封管を硝子ヤスリを用いて活け100ミリリツ
トルビーカーに移し10ミリリンドルのテトラヒドロフ
ランを刃口えて溶り干シ、し祠タ合剤浴7夜とする。
Transfer the monopodal powder to a 100ml beaker and add 33
.. Dissolve the catalyst in 4 milliliters of tetrahydrofuran and add 165 microliters of activator using a microsyringe to make a single bath solution.
Initiator) Using a glass file, transfer the sealed tube to a 100 ml beaker, add 10 ml of tetrahydrofuran to the tip, dissolve and dry, and leave in a sagittarium mixture bath for 7 nights.

開始剤溶液中にポリエステル繊維束を浸漬した後、引き
上げてドライボックス予備室中に持込み。
After immersing the polyester fiber bundle in the initiator solution, it was pulled up and brought into the dry box preparation room.

2ミリメートル水銀柱以下で減圧脱気し乾燥した後、単
量体溶液中に反偵して1時間放置する。ポリエステル繊
維毛束を単量体溶液がら取出した後、200ミリリット
ルビーカー中で100ミリリットルのテトラヒドロフラ
ンで撹拌洗浄し、ドライボックスより取出す。十分に水
洗した後摂氏40度、水銀柱3ミリメートル以下で24
時間以上真空乾燥する。この場合、T合央脈に使用した
開始剤の濃度は単量体に対して2モルパーセント、活性
吐剤濃度は同じく単量体に対して1モルパーセントとな
り溶媒(テトラヒドロフラン)のA′L]1−1一体に
対するモル分率は5と云うことになる。
After drying by degassing under 2 mm of mercury or less, it is poured into a monomer solution and left for 1 hour. After removing the polyester fiber bundle from the monomer solution, it is stirred and washed with 100 ml of tetrahydrofuran in a 200 ml beaker, and then taken out from the dry box. 24 at 40 degrees Celsius and less than 3 mm of mercury after thorough washing.
Vacuum dry for more than an hour. In this case, the concentration of the initiator used in the T central vein is 2 mole percent based on the monomer, the concentration of the active emetic agent is also 1 mole percent based on the monomer, and the concentration of the solvent (tetrahydrofuran) is A'L]1 The mole fraction relative to -1 is 5.

次に以上の如き処3jly ?し1こポリエステル繊維
毛と例等処理を施してないポリエステル繊維毛とを用い
て全く同じ仕様の細筆を各10本ずつ試作し、読取限1
u O,1ミ!Iグラムの直示型化学天性を用いて乾燥
状態に於ける車の重量、筆穂の部分に水を含ませたとき
の追の重量、走穂に含んだ水をvl(紙上に:lin 
<吸いとらせた後の−iの重量を秤量し、イ1、偲が実
際に含んだ水の重量と、その中で濾紙上へ移行した水の
重量とを算出し、それぞれ吸水量及び離水量として算術
平均するとともに確率誤差を求めたところ実施例の処理
を施したポリエステル4>−15を型素材よりなるii
) (1)吸水量は8.91±0.29ミリグラムであ
り離水量は3.41±0.36 ミ’)グラムであった
のに対し、何の処理も施し【ないポリエステルt′a維
毛素材よりなる筆の吸水量は7.41±0.25 ミリ
グラムであり離水量は2.28±0.16 ミIJグラ
ムで1 あった。
Next, 3jly like the above? Using 10 polyester fiber bristles and untreated polyester fiber bristles, we made 10 prototypes of fine brushes with exactly the same specifications, and achieved a reading limit of 1.
u O, 1 mi! Using I-gram's direct chemical nature, we can calculate the weight of the car in a dry state, the additional weight when the tip is soaked with water, and the water contained in the tip (vl (on paper: lin).
<Weigh the weight of -i after absorbing it, calculate the weight of the water actually contained in i1, and the weight of the water that has migrated onto the filter paper, and calculate the amount of water absorbed and released, respectively. The arithmetic mean of the amount of water and the probability error were determined.
) (1) The water absorption amount was 8.91 ± 0.29 milligrams and the water separation amount was 3.41 ± 0.36 micrograms, whereas the polyester t'a fiber without any treatment The amount of water absorbed by the brush made of hair material was 7.41±0.25 milligrams, and the amount of water separation was 2.28±0.16 milliJ grams.

従って吸水量を墨汁を含み得る量とし離水量な華記し得
る量と考えると、以上の如き処理を施したポリエステル
繊維毛による重鎖は処理を施していな℃・ものと較べて
、実際に墨汁を含み得る量に於て約20パーセント、墨
切れを起さず組記し得る程度に於て約50パーセント改
善されたことになり、これらの値は獣毛による毛筆に近
℃・か又は同程度であることを意味する。更に別に重合
して得られた上記双環オキサラクタムのポリマーを2.
2.2−トリフルオロエタノールに溶解した溶液中にポ
リエステル繊維毛を一本ずつ浸漬し、一本ずつ乾燥して
得た繊維毛を束として上記と同じ仕様の筆を試作し、上
記と同じ試験をしてみたところ、吸水jj、lは8.8
9±0.21ミリグラムで離水量は2.95+0.11
ミリグラムで、上記実施例の処理をしたポリエステル繊
維毛による値と同じ値を示した。
Therefore, if we consider the amount of water absorption to be the amount that can contain India ink and the amount of water repellency that can be expressed, the heavy chains made of polyester fibers treated as described above actually absorb ink This results in an improvement of about 20% in the amount of ink that can be contained, and an improvement of about 50% in the ability to type without cutting out the ink, and these values are close to or on the same level as brushes made of animal hair. It means that. Furthermore, the above-mentioned bicyclic oxalactam polymer obtained by separate polymerization was subjected to 2.
2.2-Polyester fiber bristles were dipped one by one in a solution dissolved in trifluoroethanol, dried one by one, and the obtained fiber bristles were bundled together to make a trial brush with the same specifications as above, and the same test as above was carried out. When I tried this, the water absorption jj, l was 8.8
9±0.21 milligrams and the amount of syneresis is 2.95+0.11
In milligrams, it showed the same value as the polyester fiber treated in the above example.

ここで実施例の処理を施したポリエステル挿維毛の表面
には実際にポリ双環オキサラクタムの層が形成されてい
るか否かに就でであるが、外観上は実施例の処理を施し
たものも施さなかったものも区別をつけ畑(、唯感触に
於てのみ笑カ&例の処理を雄したポリエステル繊維毛は
雨天の場合は晴天の場合と違って明らかに絡み付き易℃
・性質を示していた。従って単に外観上からは表面にポ
リ双環オキサラクタム層が形成しているか否かは断定し
難いが実施例に於ける単量体も開始剤も活性化剤もテト
ラヒドロフラン及び水には容易に溶解し、ポリ双環オキ
サラクタムはそのいずれにも溶解しないと云うことと吸
水量及び離水量がポリ双環オキサラクタムの層を実際に
形成したものの値と同じ値を示したと云うことから効果
の上では実際にポリ双環オキサラクタムの層を形成して
いると解釈される。
Here, it is unclear whether a layer of polybicyclic oxalactam is actually formed on the surface of the polyester filament bristles treated in the example, but from the appearance it appears that the polyester fiber inserts treated in the example are The polyester fibers treated with the above treatment are clearly more likely to get tangled in rainy weather than in sunny weather.
・It showed characteristics. Therefore, it is difficult to determine whether a polybicyclic oxalactam layer is formed on the surface simply from the appearance, but the monomer, initiator, and activator in the examples are easily soluble in tetrahydrofuran and water. However, since polybicyclic oxalactam does not dissolve in any of them, and the amount of water absorption and water separation was the same as that of the layer of polybicyclic oxalactam that was actually formed, it was found to be effective. It is interpreted that it actually forms a layer of polybicyclic oxalactam.

又、実施例の処理を施したポリエステル繊KIi毛と処
理を施す前の同じポリエステル伜維毛とを示差走査熱量
計(、DSC)を用(・て、その結合水及び吸湿量を測
足したところ下表の辿りであった。
In addition, the amount of bound water and moisture absorption was measured using a differential scanning calorimeter (DSC) for the KIi polyester fiber treated in the example and the same polyester fiber before treatment. The results were as shown in the table below.

処理前  0.6係   1.5係   6.8≠  
 0.7%fl) : 12時間後測定  f2) :
 48時11J1後71111定この結果から実施例の
処理な旌したポリエステル株KB毛は処理・を施さなか
ったものと較べて■明らか((高℃・吸α量を示し■結
合水は約5倍の含南率を示している。
Before processing 0.6 section 1.5 section 6.8≠
0.7%fl): Measured after 12 hours f2):
71111 after 48:11 J1 From these results, it is clear that the treated polyester strain KB wool of the example has approximately 5 times the amount of bound water compared to the untreated one. It shows the southern inclusion rate of .

次に実施例の処理を施したポリエステル繊X4Z毛の表
面にポリアミドが存在すると仮定するならば末端アミン
がニンヒドリン反応を呈するであろうと仮定してンヱイ
・ノットアンドブイ・pスバッハ(J、Knott a
nd V、Rossbach ) 、 7ンゲバンテマ
クpモレキユラーヘミ−(Angew、 Makrom
o ]、 chem、、)86巻203−213頁(1
9’80 ) r=ニンヒドリンよるポリアミド6及び
6,6中のアミン末端基の定irc、 Jの方法でニン
ヒドリンを用いて試験したところ、処理を施さなかった
ものは何等発色を示さなかったが実施例の処理を施した
ポリエステル繊維毛は明瞭に発色していた、このことは
水及びテトラヒドロフランに不瘍なニンヒドリン反応に
対して陽性な、即ちアミンを官能基として有する化合物
が実施例の処理を施したポリニスデルirgA s+L
には存在することを意味する。
Next, assuming that polyamide exists on the surface of the polyester fiber
nd V, Rossbach), 7 Ngevantemakp Molecular Hemi (Angew, Makrom)
o ], chem, ), Vol. 86, pp. 203-213 (1
9'80) r = Determination of amine end groups in polyamide 6 and 6,6 by ninhydrin IRC, When tested using ninhydrin according to the method of J, the untreated product did not show any color development, but it was not carried out. The polyester fiber treated in the example was clearly colored, which indicates that the compound that is positive for the ninhydrin reaction, which is insensitive to water and tetrahydrofuran, and has an amine as a functional group, was treated in the example. Polynisdel irgA s+L
means that it exists.

従ってこの場合実施例の反応機構その他の因子が町成り
明4′6なものであり、反応の前後に於て不確定な要素
が入り込む余地がな℃・ので実施例の処理を施したポリ
エステル繊維毛の衣l■]にはポリ双環オキサラクタム
が形成されていることを意味する。
Therefore, in this case, the reaction mechanism and other factors in the example are well known, and there is no room for uncertain factors to enter before and after the reaction. Therefore, the polyester fiber treated in the example is This means that polybicyclic oxalactam is formed in the coat of hair.

更に本発明による方法が効果的に発揮されるのは重合反
応に於て生成する重合体が単量体溶液に不R4で沈澱と
なって生成してくるような謂ゆる不均一系重合に於てで
あることが前提条件であって重合反応性の大小にはあま
り影響を受けな℃・と考えられる。従って実施例の場合
は重合反応性の大きな双環オキサラクタムを用いて1時
1ijl 0)′i!合時開時間ったが重合反応性のよ
り小さ℃・2−ピロリドン、ε−カプロラクタムなどに
於ても正合時1jlをより長くすればよいことになる。
Furthermore, the method according to the present invention is effectively exhibited in so-called heterogeneous polymerization in which the polymer produced in the polymerization reaction is precipitated with R4 in the monomer solution. It is considered that the prerequisite is that the polymerization temperature is ℃・, which is not affected much by the magnitude of the polymerization reactivity. Therefore, in the case of the example, a bicyclic oxalactam with high polymerization reactivity was used and 1 ijl 0)'i! Although the opening time was longer during the polymerization, it is sufficient to make the 1jl longer during the polymerization even in the case of C. 2-pyrrolidone, ε-caprolactam, etc., which have lower polymerization reactivity.

この場合塊状重合となり2−ピロリドンの場合は重合温
度を摂ダ 氏40度附近とし、ε−カプロラクタムは摂氏130度
以上としなげればならな℃・、℃・すれの場合も不拘−
呆で重合は進行する。
In this case, bulk polymerization occurs, and in the case of 2-pyrrolidone, the polymerization temperature must be around 40 degrees Celsius, and in the case of ε-caprolactam, it must be at least 130 degrees Celsius.
Polymerization proceeds in a daze.

次に本発明による方法はラクタムのアニオン重合にのみ
適用され得るのではなくアクリルスチレン、ブタジェン
などのビニル七ツマ−のラジカル重合、オレフィン、ビ
ニルエーテル、スチレン誘導体、ジエン類、カルボニル
化合物、環状ニスフルなどのカチオン重合、アニオン重
合などにも炉用することができ、形成しようとする合成
Jl;; 脂/dも現水性、疎水性ばかりでなく接尤住
、撥水性、(骨性など目的に応じた性質を有するものと
することができる。
Next, the method according to the present invention can be applied not only to the anionic polymerization of lactams, but also to the radical polymerization of vinyl polymers such as acrylstyrene and butadiene, olefins, vinyl ethers, styrene derivatives, dienes, carbonyl compounds, cyclic nisfuls, etc. The furnace can be used for cationic polymerization, anionic polymerization, etc., and the synthetic Jl/d to be formed has not only hydrophobicity and hydrophobicity, but also adhesion, water repellency, (osseousness, etc.) depending on the purpose. It can be made to have a property.

従って本発明による方法は、最近注目され始めたプラズ
マ重合方法が乾式の謂ゆるプラズマ又は紫外線を用いて
物質の表面に化学反応を起させることにより表面を改質
しようとするものであるのに対し最初物質の表面に重合
触媒を存在させ、次で単量体を存在させることにより物
質の触媒が存在する表面だけに重合を進行させ、結果と
して表面が希望する重合体の性質を有する物質を生産す
る方法であり従来の既に確立された高分子合成の学問体
系を基礎としたものである。
Therefore, the method according to the present invention is different from the plasma polymerization method, which has recently begun to attract attention, which attempts to modify the surface of a material by causing a chemical reaction on the surface of the material using dry plasma or ultraviolet rays. First, a polymerization catalyst is present on the surface of the substance, and then a monomer is present, so that polymerization proceeds only on the surface of the substance where the catalyst is present, resulting in the production of a substance whose surface has the desired polymer properties. It is a method based on the conventional academic system of polymer synthesis that has already been established.

本発明による表面の改質された物質を生産する方法ハ、
従ってプラズマ重合方法とその目的及び効果に於て一部
重複する可能性の強いものであって利用範凹の広い画期
的な技術的思想の創作であると思う。
A method for producing a surface-modified material according to the present invention; c.
Therefore, there is a strong possibility that the plasma polymerization method and its purpose and effects may overlap in part, and I believe that this is the creation of an epoch-making technical idea that can be used in a wide range of applications.

時計出願人  株式会社 新和製作所Watch applicant: Shinwa Seisakusho Co., Ltd.

Claims (1)

【特許請求の範囲】 1)重合が不均一系で進行する重合系に於て、重合触媒
の溶液中に表面を改質しようとするものを浸漬し、引き
上げ−〔乾燥することにより改質しようとする物の表面
、に薄く固体の重合触媒を存在させた後、単量体溶ぽ中
に浸漬して重合を進行させ、重合体以外を浴解し抽出す
る溶液中に浸漬して!41拌洗浄し、乾燥することによ
り表面に合成樹脂膜を形成させることを%CIJと子る
表面の改質された物質を生産する方法。 2)表面を改質しようとする物がテーパー状ニ先鋭化さ
れたポリエステル繊維毛であり、単fti体溶液はラク
タム及び触媒量のN−7シルラクタムなる活性化剤とよ
りなる溶液であり、重合触媒はラクジ′ムのアルカリ金
17A塩なるi3N始剤であり、乾燥窒素気流下で処理
が行われる特許請求の範囲第1項記載の表面の改質され
た物質を生産する方法。
[Claims] 1) In a polymerization system in which polymerization proceeds in a heterogeneous system, an object whose surface is to be modified is immersed in a solution of a polymerization catalyst, pulled out, and then dried. After making a thin solid polymerization catalyst exist on the surface of the object, it is immersed in a monomer solution to proceed with polymerization, and then immersed in a solution that decomposes and extracts substances other than the polymer. 41 A method for producing a surface-modified material that involves forming a synthetic resin film on the surface by stirring, washing, and drying. 2) The material whose surface is to be modified is tapered sharpened polyester fiber hair, and the single FTI solution is a solution consisting of a lactam and a catalytic amount of an activator called N-7 sillactam. 2. A method for producing a surface-modified material as claimed in claim 1, wherein the catalyst is an i3N initiator consisting of an alkali gold 17A salt of laczim, and the treatment is carried out under a stream of dry nitrogen.
JP7223183A 1983-04-26 1983-04-26 Production of surface modified substance Pending JPS59199863A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7223183A JPS59199863A (en) 1983-04-26 1983-04-26 Production of surface modified substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7223183A JPS59199863A (en) 1983-04-26 1983-04-26 Production of surface modified substance

Publications (1)

Publication Number Publication Date
JPS59199863A true JPS59199863A (en) 1984-11-13

Family

ID=13483284

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7223183A Pending JPS59199863A (en) 1983-04-26 1983-04-26 Production of surface modified substance

Country Status (1)

Country Link
JP (1) JPS59199863A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014156935A1 (en) * 2013-03-28 2014-10-02 日本ゼオン株式会社 Apparatus for producing long resin complex, and method for producing long resin complex
US9186852B2 (en) 2013-11-22 2015-11-17 Johns Manville Fiber-containing prepregs and methods and systems of making
US10717245B2 (en) 2018-04-03 2020-07-21 Johns Manville System for producing a fully impregnated thermoplastic prepreg
US10857744B2 (en) 2018-04-03 2020-12-08 Johns Manville System for producing a fully impregnated thermoplastic prepreg
US11548245B2 (en) 2013-11-22 2023-01-10 Johns Manville Fiber-containing prepregs and methods and systems of making

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS503839A (en) * 1973-05-12 1975-01-16

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS503839A (en) * 1973-05-12 1975-01-16

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014156935A1 (en) * 2013-03-28 2014-10-02 日本ゼオン株式会社 Apparatus for producing long resin complex, and method for producing long resin complex
US9186852B2 (en) 2013-11-22 2015-11-17 Johns Manville Fiber-containing prepregs and methods and systems of making
US11548245B2 (en) 2013-11-22 2023-01-10 Johns Manville Fiber-containing prepregs and methods and systems of making
US10717245B2 (en) 2018-04-03 2020-07-21 Johns Manville System for producing a fully impregnated thermoplastic prepreg
US10857744B2 (en) 2018-04-03 2020-12-08 Johns Manville System for producing a fully impregnated thermoplastic prepreg
US11458696B2 (en) 2018-04-03 2022-10-04 Johns Manville System for producing a fully impregnated thermoplastic prepreg

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